Injection blow moulded single layer metallocene polyethylene container

ABSTRACT

A single layer hollow packaging, comprising essentially a metallocene-produced polyethylene and produced by injection blow moulding, chasacterised in that said hollow packaging has an external and internal gloss of at least 30 and said metallocene-produced polyethylene has a density of from 0.910 up to 0.966 g/CM3 or up to homopolymer densities and a melt index MI2 of from 0.5 to 2.5 g/10 min.

This invention is related to hollow packagings having improved optical properties and in particular to the production of high gloss bottles, jars, etc. formed of polyethylene by injection blow moulding.

Several methods have been sought to produce high gloss bottles presenting good processability and good mechanical properties but all the blends and techniques used so far present various disadvantages.

High gloss high density polyethylene (HDPE) has been used: it is characterised by a very narrow molecular weight distribution that is typically inferior to 8. The molecular weight distribution can be completely defined by means of a curve obtained by gel permeation chromatography. Generally, the molecular weight distribution (MWD) is more simply defined by a parameter, known as the dispersion index D, which is the ratio between the average molecular weight by weight (Mw) and the average molecular weight by number (Mn). The dispersion index constitutes a measure of the width of the molecular weight distribution. It is known that a resin of narrow molecular weight distribution will produce plastic containers of very high gloss but simultaneously, that such resin will be very difficult to process and will be characterised by very poor mechanical properties. It has also been observed that said resins have poor mechanical properties, particularly, a very low environmental stress crack resistance (Modern Plastic International, August 1993, p. 45).

The coextrusion of high density polyethylene (HDPE) with a thin external layer of polyamide has been used to produce bottles of very high gloss but that method suffers the major drawback of necessitating an adhesive layer between the HDPE and the polyamide layers.

The coextrusion of high density polyethylene and an external layer of low density polyethylene leads to bottles with a fair gloss. These bottles however have an unpleasant greasy touch and offer a very poor resistance to scratching.

In another method, disclosed in co-pending European Patent Application n^(o) 00201155.9, high gloss plastic containers comprise an internal layer including a polyolefin and an external layer including a styrenic component containing from 40 to 85 wt % of styrene, based on the weight of the external.

There is thus a need for a method for efficiently producing hollow packagings of very high gloss as well as good processability and mechanical properties by injection moulding.

An aim of the present invention is to produce hollow packagings that offer simultaneously the desired glossy appearance and a good resistance to scratching.

It is also an aim of the present invention to obtain glossy hollow packagings with good processability and good mechanical properties.

The present invention provides single layer hollow packagings, which consist essentially of metallocene-produced polyethylene having a density of from 0.915 g/cm³, preferably from 0.925 g/cm³ up to 0.966 g/cm³, or up to homopolymer densities, and a melt index MI2 of from 0.2 to 5 g/10 min, preferably of from 0.5 to 2.5 g/10 min, and most preferably of from 0.5 to 2 g/10 min, characterised in that said hollow packagings are produced by injection blow moulding and have an external and internal gloss of at least 30.

In this specification, the density of the polyethylene is measured at 23° C. using the procedures of ASTM D 1505.

The melt index MI2 is measured using the procedures of ASTM D 1238 at 190° C. using a load of 2.16 kg. The high load melt index HLMI is measured using the procedures of ASTM D 1238 at 190° C. using a load of 21.6 kg.

A number of different metallocene catalyst systems have been disclosed for the manufacture of polyethylene, in particular medium-density polyethylene (MDPE) and high-density polyethylene (HDPE) suitable for injection blow moulding. It is known in the art that the physical properties, in particular the mechanical properties, of a polyethylene product vary depending on what catalytic system was employed to make the polyethylene

The HDPE can be polymerised with a metallocene catalyst system capable of producing a mono- or bi- or multimodal distribution, either in a two step process such as described for example in EP-A-0,881,237, or as a dual or multiple site catalyst in a single reactor such as described for example in EP-A-0,619,325. Any metallocene catalyst known in the art can be used in the present invention. It is represented by the general formula: (CP)_(m)MR_(n)X_(q)  I. wherein Cp is a cyclopentadienyl ring, M is a group 4b, 5b or 6b transition metal, R is a hydrocarbyl group or hydrocarboxy having from 1 to 20 carbon atoms, X is a halogen, and m-1-3, n=0-3, q=0-3 and the sum m+n+q is equal to the oxidation state of the metal. (C₅R′_(k))_(g)R″_(s)(C₅R′_(k))MQ_(3-g)  II. R″_(s)(C₅R′_(k))₂MQ′  III. wherein (C₅R′_(k)) is a cyclopentadienyl or substituted cyclopentadienyl, each R′ is the same or different and is hydrogen or a hydrocarbyl radical such as alkyl, alkenyl, aryl, alkylaryl, or arylalkyl radical containing from 1 to 20 carbon atoms or two carbon atoms are joined together to form a C₄-C₆ ring, R″ is a C₁-C₄ alkylene radical, a dialkyl germanium or silicon or siloxane, or a alkyl phosphine or amine radical bridging two (C₅R′_(k)) rings, Q is a hydrocarbyl radical such as aryl, alkyl, alkenyl, alkylaryl, or aryl alkyl radical having from 1-20 carbon atoms, hydrocarboxy radical having 1-20 carbon atoms or halogen and can be the same or different from each other, Q′ is an alkylidene radical having from 1 to about 20 carbon atoms, s is 0 or 1, g is 0, 1 or 2, s is 0 when g is 0, k is 4 when s is 1 and k is 5 when s is 0, and M is as defined above.

Among the preferred metallocenes used in the present invention, one can cite among others ethylene bis-(tetrahydroindenyl) zirconium dichloride, ethylene bis-(indenyl) zirconium dichloride or bis-(n-butylcyclopentadienyl) zirconium dichloride mono-, di- or tri-substituted as disclosed for example in EP-A-870,048.

The metallocene may be supported according to any method known in the art. In the event it is supported, the support used in the present invention can be any organic or inorganic solids, particularly porous supports such as talc, inorganic oxides, and resinous support material such as polyolefin. Preferably, the support material is an inorganic oxide in its finely divided form.

An active site must be created by adding an activating agent having an ionising action.

Preferably, alumoxane is used as activating agent during the polymerization procedure, and any alumoxane known in the art is suitable.

The preferred alumoxanes comprise oligomeric linear and/or cyclic alkyl alumoxanes represented by the formula:

for oligomeric, linear alumoxanes, and

for oligomeric, cyclic alumoxanes, wherein n is 1-40, preferably 10-20, m is 3-40, preferably 3-20 and R is a C₁-C₈ alkyl group and preferably methyl.

Methylalumoxane is preferably used.

When alumoxane is not used as a cocatalyst, one or more aluminiumalkyl represented by the formula AIR_(x) are used wherein each R is the same or different and is selected from halides or from alkoxy or alkyl groups having from 1 to 12 carbon atoms and x is from 1 to 3. Especially suitable aluminiumalkyl are trialkylaluminium, the most preferred being triisobutylaluminium (TIBAL).

The metallocene catalyst utilised to produce a polyethylene, as required for preparing the high gloss hollow packagings of the present invention, can be used in gas, solution or slurry polymerisation. Preferably, the polymerization process is conducted under slurry phase polymerization conditions. The polymerisation temperature ranges from 20 to 125° C., preferably from 60 to 95° C. and the pressure ranges from 0.1 to 5.6 Mpa, preferably from 2 to 4 Mpa, for a time ranging from 10 minutes to 4 hours, preferably from 1 and 2.5 hours).

It is preferred that the polymerization reaction be run in a diluent at a temperature at which the polymer remains as a suspended solid in the diluent.

A continuous loop reactor is preferably used for conducting the polymerisation. Multiple loop reactors can also be used.

The average molecular weight is controlled by adding hydrogen during polymerisation. The relative amounts of hydrogen and olefin introduced into the polymerisation reactor are from 0.001 to 15 mole percent hydrogen and from 99.999 to 85 mole percent olefin based on total hydrogen and olefin present, preferably from 0.2 to 3 mole percent hydrogen and from 99.8 to 97 mole percent olefin.

The density of the polyethylene is regulated by the amount of comonomer injected into the reactor; examples of comonomer which can be used include 1-olefins butene, hexene, octene, 4-methyl-pentene, and the like, the most preferred being hexene.

The densities of the polyethylenes required for preparing the hollow packagings of the present invention range from 0.915 g/cm³, preferably from 0.925 g/cm³ up to 0.966 g/cm³, or up to homopolymer densities.

The melt index of polyethylene is regulated by the amount of hydrogen injected into the reactor. The melt indexes useful in the present invention range from 0.2 to 5 g/10 min and preferably from 0.5 g/10 min to 2.5 g/10′ min.

The polyethylene resin used in the present invention can be prepared with either a single site metallocene catalyst or with a multiple site metallocene catalyst and it has therefore either a monomodal or a bimodal molecular weight distribution. The molecular weight distribution is of from 2 to 20, preferably, of from 2 to 7 and more preferably of from 2 to 5.

The polyethylene resins produced in accordance with the above-described processes have physical properties making them particularly suitable for use as injection blow moulding grade polyethylenes. In addition, it has surprisingly been observed that they have excellent processability even when their molecular weight distribution is narrow.

The polyethylene resins of the present invention are used preferably for producing containers of a capacity ranging from 0.0005 to 2 I. They are more preferably used for producing food packaging, such as for example milk bottles or juice bottles, cosmetic or pharmaceutical packaging and household packaging.

The injection moulding machine, can be any one of the machines generally used for injection-blow-moulding, such as for example the JOMAR and UNILOY machines. They are continuous injection-blowing-ejection machines with up to 16 injection-blowing dies that can be used for the production of polyethylene containers of up to 0.8 litre capacity.

The hollow packagings of the present invention are characterised by a very high gloss for both inner and outer surfaces, as measured using the ASTM D 2457-90 test, a low haze as measured by ASTM D 1003-92, and an outstanding resistance to drop. In addition, because of the very smooth inner surfaces, it is possible to increase the pouring speed and to decrease the amount of residue left in the packaging.

The impact strength was measured on moulded plates at −30° C. following the method of standard test ISO 8256.

Additionally and quite surprisingly, the production rate is very high even though the melt index is low. The process is very stable and the packagings are produced with an excellent success rate.

EXAMPLES

Several polyethylene resins were prepared and tested for gloss, haze, impact strength and drop.

Resin R1.

The polyethylene resin R1 was obtained by continuous polymerisation in a loop slurry reactor with a supported and ionised metallocene catalyst prepared in two steps by first reacting SiO₂ with MAO to produce SiO₂.MAO and then reacting 94 wt % of the SiO₂.MAO produced in the first step with 6 wt % of ethylene bis-(tetrahydroindenyl) zirconium dichloride. The dry catalyst was slurried in isobutane and pre-contacted with triisobutylaluminium (TIBAI, 10 wt % in hexane) before injection in the reactor. The reaction was conducted in a slurry loop reactor with the polymerisation temperature being maintained at 90° C. The operating conditions were as follows:

-   -   TIBAI conc (ppm): 100-200     -   iC4 feed (kg/h): 1940     -   C2 feed (kg/h): 3900     -   C6 feed (g/kg C2): 22     -   H2 feed (g/t): 42         Wherein, C2 is ethylene, C6 is 1-hexene, iC4 is isobutane and         TIBAI is triisobutylaluminium.         Resin R2.

The polyethylene resin R2 was prepared following the same procedure as that used for polymerising resin R1 except that the metallocene catalyst was bis-(butylcyclopentadienyl) zirconium dichloride. The cocatalyst was also TIBAI (10 wt % in hexane) and the polymersation temperature was 90° C. The operating conditions were as follows:

-   -   IC4 feed (kg/h): 24     -   C2 feed (cc/h): 9     -   C6 feed (cc/h): 27     -   H2 feed (NI/h): 1.9     -   TIBAI conc (ppm): 292         Resin R3.

Resin R3 is a monomodal polyethylene resin produced with a chromium catalyst, commercialised under the name ®Finathène 5502: it was prepared with a supported chromium catalyst.

Resin R4.

Resin R4 is a low density polyethylene resin, produced by Dupont under the name ®DuPont 20-6064 for applications in injection blow moulding.

The resins R1 to R3 were prepared with hexene as comonomer.

The properties of these resins are summarised in Table I. The impact strength was measured on moulded plates, at a temperature of −30° C. and following the method of standard test ISO 8256. TABLE I HLMI MI2 Imp. Str. Resin Density g/cm³ g/10′ g/10′ Mn Mw Mz kj/m² MWD R1 0.934 25.1 0.96 34083 88134 167888 170 2.6 R2 0.950 27 1.6 34624 92729 201616 130 2.7 R3 0.953 17.65 0.19 19620 153558 1333100 80 7.8 R4 0.92 n.a. 1.9 n.a. n.a. n.a. n.a. n.a. n.a.: not available

Resins R1 and R3 were injection-blow-moulded with the UNILOY injection-blowing machine under the processing conditions summarised in Table II.

Resins R2 and R4 were processed with the injection-blow-moulding (IBM) machine, 15 model available from Jomar. The injection blow moulding process is divided into three steps:

-   -   1. the injection step, wherein the molten polymer is injected         through nozzles into heated preform moulds forming the external         shape, said moulds being clamped around core rods forming the         internal shape;     -   2. the blowing step wherein the core rods allow compressed air         into the preforms that inflate to the shape of the chilled blow         moulds; and     -   3. the ejection step wherein after a cooling period, the         finished article is stripped off the core rod.

The machine and mould characteristics are summarised in Table III. The general purpose mixing screw has a diameter of 25.4 mm and a length to diameter ratio L/D of 30:1.

The extruded articles all exhibit a very high gloss and an excellent impact strength. TABLE II Mass Cycle Int. gloss Ext. gloss Temp. time 60° 60° Resin ° C. S % % R1 200-210 16.49 72 38 R2 210-220 15.07 n.a. 62 R3 230-240 19.30 20 22 R4 180-200 15.13 n.a. n.a. n.a.: not available

During processing, resins R1 and R2 showed a very high process-stability, a very high percentage of well-formed bottles, a good weight consistency. The bottles obtained were very glossy as compared to those obtained with resins R3 and R4. This can be clearly seen in FIG. 1 representing bottles prepared by injection blow moulding respectively with a low-density polyethylene produced with the metallocene catalyst ethylene bis(tetrahydroindenyl)zirconium dichloride and a low-density polyethylene produced by Dupont and in FIG. 2 representing bottles prepared by injection blow moulding respectively with a medium-density polyethylene produced with the metallocene catalyst ethylene bis(tetrahydroindenyl)zirconium dichloride and a medium-density polyethylene produced with a chromium catalyst. TABLE III Preform clamp @ 141 kg/cm² (tons) 11.4 Casting area @ 246 kg/cm² (cm²) 46 @ 387 kg/cm² (cm²) 29 Blow mould clamp @ 141 kg/cm² (tons) 2.9 Shut height (mm) 203.2 Press stroke (mm) 101.6 Max. die set size (mm) 254 × 286 Tigger Bar Irength mm) 166 Max. swing length (mm) 356 Shot capacity (g)^(a) 50 Motor size (kw) 15

Five additional metallocene-produced polyethylene resins, R5 to R9, were tested at Jomar facilities in the U.S.A. Resins R5 and R6 were prepared with bis(butylcyclopentadienyl) zirconium dichloride and R7 to R9 were prepared with ethylene bis(tetrahydroindenyl) zirconium dichloride.

For comparison polyethylene resin R10, prepared with a chromium-based catalyst sytem and polyethylene resin R11, prepared with a Ziegler-Natta catalyst system were also tested under similar conditions.

The properties of these resins are summarised in Table IV. TABLE IV MI2 Density Resin g/10′ g/cm³ Mn Mw Mz MWD R5 2.36 0.954 31628 80859 155635 2.6 R6 11 0.958 20417 51223 94478 2.5 R7 2.04 0.949 25937 68841 138233 2.7 R8 0.85 0.934 23882 80224 201417 3.4 R9 0.65 0.947 32034 87444 182364 2.7 R10 0.3 0.955 R11 1.2 0.962

Two different moulds were used for testing the injection blow moulding performances of these resins:

-   -   a system equipped with a four cavities 1-oz (28.35 g) shampoo         bottle mould, and     -   a system equipped with a 10 cavities 3-oz (85.05 g) round jar         mould.

The results obtained confirm the trends already observed with resins R1 to R4:

-   -   the optical properties of the metallocene-produced resins R5 to         R9 are significantly better than those of resins R10 and R11         prepared respectively with a chromium-based and a Ziegler-Natta         catalyst;     -   the cycle time of the metallocene-produced resins R5 to R9 is         significantly shorter than that of resins R10 and R11;     -   increasing the melt index MI2 of the resin decreases the cycle         time but narrows the processing window, the narrowing of the         processing window being less severe for the metallocene-based         resins R5 to R9 than for the chromium-based or         Ziegler-Natta-based resins R10 and R11;     -   resins R7 to R9 prepared with ethylene bis(tetrahydroindenyl)         zirconium dichloride have a shorter cycle time and a lower shear         visvosity (in the shear rate region of 1000 s-1) and thereby a         better processability than resins R5 and R6 prepared with         bis(butylcyclopentadienyl) zirconium dichloride;     -   resins R7 to R9 provide a better mould replication than resin R         11.

In addition, the following characteristics were evaluated for each of the 1-oz (28.35 g) bottles:

-   -   weight     -   wall thickness distribution     -   gloss     -   height     -   bottle diameter     -   neck diameter

The gloss was measured varying the melt temperature, the melt index MI2 and the mould: a polished mould and a sand-blasted mould were used.

The gloss results are presented in Table V and the other measurements are summarised in Table VI. TABLE V MI2 Melt Temp. Sand-blasted Polished Resin g/10′ ° C. mould mould R5 2.36 185 33.6 62.9 R5 2.36 215 28.8 63.4 R7 2.04 185 33.5 67.2 R8 0.85 185 25.4 71.6 R8 0.85 215 21.3 81.7 R10 0.3 215 32.1 47.9 R11 1.2 215 24.8 73

It can be concluded from Table V that for a polished mould, the optical properties improve with increasing melt temperature at similar melt index. This is due to a better mould replication as can de deduced when comparing the gloss results for the polished and sand-blasted moulds at high temperature for resin R8. Increasing the melt index reduces the optical properties as can be seen when comparing the gloss results obtained for the polished moulds with resins R7 and R8. TABLE VI Melt temp. Height Bottle diam. Neck diam. Resin ° C. Weight g mm mm mm R5 185 6.19 80.41 25.74 15.29 R5 215 6.06 80.39 25.78 15.18 R7 185 6.19 80.44 25.77 15.29 R8 185 6.1 80.27 25.76 15.27 R8 215 6.04 80.23 25.73 15.19 R10 195 — 80.43 25.83 15.36 R10 215 6.06 80.36 25.03 15.27 R11 215 6.08 80.36 25.76 15.33

It can be concluded from Table VI that the metallocene-prepared polyethylene resins R5, R7 and R8 produce bottles with smaller neck diameter than resins R10 and R11. It is also observed that lowering the melt temperature leads to a slight weight increase of the bottles.

The thickness distribution of the 1-oz (28.35 g) bottles has also been studied. For that purpose, the bottle height has been divided into four equal parts, and for each of these four heights, the thickness has been measured at four points equally spaced on the circumference of the bottle. The walls of the bottles have a thickness of about 1 mm. It has been observed that resins R5 to R9 have an excellent thickness distribution very little affected by the melt temperature and better than that obtained for the bottles produced with resins R10 and R11. It has also been observed that increasing the melt index to values above 2 g/10 min leads to poor thickness distribution for the bottles produced with metallocene-based polyethylene resins.

These results show unambiguously the improved qualities of gloss, cycle time, dimensional stability and impact strength of the hollow packagings obtained with metallocene-produced polyethylene. 

1-8. (Cancelled)
 9. A hollow, high-gloss packaging article produced by injection blow molding comprising a single layer wall structure having an external surface having a gloss of at least 30 and an internal surface having a gloss of at least 30 and defining an internal chamber, said wall structure formed of a single layer of a metallocene produced-polyethylene having a density of from 0.910 to 0.966 g/cm³ and a melt index MI2 of from 0.2 to 5 g/10 min.
 10. The hollow packaging article of claim 9 wherein said metallocene-produced polyethylene has a melt index MI2 of from 0.5 to 2.5 g/10 min.
 11. The hollow packaging article of claim 9, wherein the metallocene-produced polyethylene has a melt index M12 of from 0.5 to 2.0 g/10 min.
 12. The hollow packaging article of claim 9 wherein the metallocene-produced polyethylene has a melt index M12 of from 0.5 to 2.0 g/10 min.
 13. The hollow packaging article of claim 9 wherein said metallocene-produced polyethylene has a density within the range of 0.925 g/cm³ to 0.966 g/cm³.
 14. The hollow packaging article of claim 9 wherein said metallocene-produced polyethylene is produced by the polymerization of ethylene in the presence of a metallocene catalyst selected from the group consisting of ethylene bis-(tetrahydroindenyl) zirconium dichloride, ethylene bis-(indenyl) zirconium dichloride, and bis-(n-butylcyclopentadienyl) zirconium dichloride.
 15. The hollow packaging article of claim 9 wherein the metallocene-produced polyethylene has a molecular weight distribution within the range of 2-5.
 16. The hollow packaging article of claim 9 wherein said single layer wall structure is configured to define a chamber to provide a container for a liquid product.
 17. The hollow packaging article of claim 9 wherein said single layer wall structure is configured to define a chamber to provide a container for a food product.
 18. The hollow packaging article of claim 9 wherein said single layer wall structure is configured to define a chamber to provide packaging suitable for cosmetic or pharmaceutical products.
 19. The hollow packaging article of claim 9 wherein said polyethylene is a co-polymer of ethylene and a higher molecular weight alpha olefin.
 20. The hollow packaging article of claim 19 wherein said alpha olefin is selected from the group consisting of butene, hexene, octene and 4-methyl pentene.
 21. The hollow packaging article of claim 20 wherein said higher molecular weight alpha olefin is hexene.
 22. The hollow packaging article of claim 9 wherein said single layer wall structure is formed of a metallocene-produced polyethylene homopolymer. 